Measuring and modelling the glucose-fermenting activity of Lactobacillus plantarum

Summary The pH decrease in a phosphate buffer due to fermentation of glucose to lactic acid by non-growing Lactobacillus plantarum cells has been studied. The method used offers a quick and reproducible way of measuring the glucose-fermenting activity of L. plantarum. The maximum observed velocity of pH decrease is linear with the biomass concentration and is defined as the activity of the cell suspension. With L. plantarum, recalculation of this arbitrary unit (pH·min^–1 per gram dry weight) to a conceivable unit of lactic acid production rate (mol·min^–1 per gram dry weight) is possible. This recalculation is based on the titration theory of a weak base with a weak acid. The same theory together with the lactic acid production kinetics of L. plantarum is applied to model the entire pH-time curve.Offprint requests to: L. C. Lievense     

Acid Sensitivity of a Mutant of Lactococcus lactis subsp. lactis C2 with Reduced Membrane-bound ATPase Activity

Mutants with reduced membrane-bound ATPase activities were isolated from Lactococcus lactis subsp. lactis C2 as spontaneous neomycin-resistant mutants. Characteristics of the representative mutant, No. 1016–51, were compared with the parental strain in cultures using a jar fermentor with the pH controlled at various values. At pH 6.5, the fermentation patterns, i.e., glucose consumption, growth, and lactic acid production, of both strains appeared identical. At pH 4.5, however, the levels of growth, lactic acid production, and the amounts of lactic acid produced per cell after the culture for 24 h decreased to 60, 36, and 60% of the parental strain, respectively. During the cultures at pH 6.5, no differences were found in viabilities between both strains even after 80 h. On the other hand, at pH 4.0, the viable count of the strain No. 1016–51 in a 72-h culture decreased to less than 1% of that of the zero time, while the parental strain maintained its original viability. Therefore, it was concluded that the membrane-bound ATPase is essential for this organism to survive at low pH, probably through its function of proton pumping for maintaining cytoplasmic pH levels.     

Physiological and fermentation properties of <Emphasis Type="Italic">Bacillus coagulans</Emphasis> and a mutant lacking fermentative lactate dehydrogenase activity

Bacillus coagulans, a sporogenic lactic acid bacterium, grows optimally at 50–55°C and produces lactic acid as the primary fermentation product from both hexoses and pentoses. The amount of fungal cellulases required for simultaneous saccharification and fermentation (SSF) at 55°C was previously reported to be three to four times lower than for SSF at the optimum growth temperature for Saccharomyces cerevisiae of 35°C. An ethanologenic B. coagulans is expected to lower the cellulase loading and production cost of cellulosic ethanol due to SSF at 55°C. As a first step towards developing B. coagulans as an ethanologenic microbial biocatalyst, activity of the primary fermentation enzyme L-lactate dehydrogenase was removed by mutation (strain Suy27). Strain Suy27 produced ethanol as the main fermentation product from glucose during growth at pH 7.0 (0.33 g ethanol per g glucose fermented). Pyruvate dehydrogenase (PDH) and alcohol dehydrogenase (ADH) acting in series contributed to about 55% of the ethanol produced by this mutant while pyruvate formate lyase and ADH were responsible for the remainder. Due to the absence of PDH activity in B. coagulans during fermentative growth at pH 5.0, the l-ldh mutant failed to grow anaerobically at pH 5.0. Strain Suy27-13, a derivative of the l-ldh mutant strain Suy27, that produced PDH activity during anaerobic growth at pH 5.0 grew at this pH and also produced ethanol as the fermentation product (0.39 g per g glucose). These results show that construction of an ethanologenic B. coagulans requires optimal expression of PDH activity in addition to the removal of the LDH activity to support growth and ethanol production.     

Inhibited growth of common enteropathogenic bacteria in lactic-fermented cereal gruels

A natural lactic fermentation of mixtures of water and whole flour of either maize or high-tannin sorghum was obtained either before or after cooking to a weaning gruel: The preparations had a final pH of about 3.8 (range 3.67 to 4.00) and a ratio of lactic acid to acetic acid of 91 (w/w). The growth of added (about 10⁷ c.f.u./g gruel) Gram-negative intestinal pathogenic bacteria, enterotoxigenicEscherichia coli, Campylobacter jejuni, Shigella flexneri andSalmonella typhimurium, was strongly inhibited in the sour gruels, and the effect could primarily be explained by the low pH caused by the formation of lactic and acetic acids during the fermentation process. Of the added Gram-positive bacteria,Bacillus cereus andStaphylococcus aureus showed similar inhibited growth up to 7h after inoculation in the sour gruels. The strain ofStaphylococcus, however, showed only a continued reduction in growth in the fermented gruel samples, which had a viable lactic bacteria culture indicating the presence of a bacteriocin. This implies that a low pH (< 4.0) alone is not sufficient to sustain the inhibition of the growth ofStaphylococcus aureus. The survival studies were carried out at optimal temperatures for each respective enteropathogen.     

Growth conditions of clostridium perfringens type B for production of toxins used to obtain veterinary vaccines

The diseases caused for Clostridium perfringens are generically called enterotoxemias because toxins produced in the intestine may be absorbed into the general circulation. C. perfringens type B, grown in batch fermentation, produced toxins used to obtain veterinary vaccines. Glucose in concentrations of 1.4–111.1 mM was used to define the culture medium. The minimum concentration for a satisfactory production of vaccines against clostridial diseases was 55.6 mM. Best results were brought forth by meat and casein peptones, both in the concentration 5.0 g l^?1 in combination with glucose and a culture pH maintained at 6.5 throughout the fermentation process. The production of lactic, acetic and propionic organic acids was observed. Ethanol was the metabolite produced in the highest concentration when cultures maintained steady pH of 6.5 with exception of cultures with initial glucose concentration of 1.4 mM, where the highest production was of propionic acid. Maximal cell concentration and the highest toxin title concomitantly low yield coefficient to organic acids and ethanol were obtained using basal medium containing 111.1 mM glucose under a controlled pH culture (pH) 6.5 in batch fermentations of C. perfringens type B. These data contribute to improve process for industrial toxin production allowing better condition to produce a toxoid vaccine.     

Ensilage characteristics of three tropical grasses as influenced by stage of growth and addition of molasses

When molasses was added during ensilage of three tropical grasses [hamil grass (Panicum maximum cv. Hamil), pangola grass (Digitaria decumbens) and setaria (Setaria sphacelata cv. Kazungula)] the final pH, concentration of fermentation acids (except lactic acid) and NH₃–N content were all similar after 100 days of incubation. Pangola grass silage had significantly higher lactic acid content (66 g/kg dry matter) than the other two. Adding either 4 or 8% (w/w) molasses reduced NH₃–N, volatile fatty acid content and pH but increased lactic acid content in the final silages. Numbers of lactic acid bacteria remained approximately constant during the course of the fermentation, although large differences were noted in the species composition of the populations. At the time of ensiling, only Pediococcus spp. and Leuconostoc spp. were detected. By 5 days, the homo-fermentative population, notably Lactobacillus plantarum, dominated (43%) and remained dominant. Hetero-fermentative rods were only detected in the 100-day silage, where they represented 29% of the strains isolated. Homo-fermenters were more abundant in pangola (60%) and setaria (47%) silages than hamil (27%) silages. Homo-fermenter populations were lowest in the 12-week forage. Molasses additions increased homo-fermenter populations. Pangola grass gave the best quality silage but, since the water-soluble carbohydrate content in the grasses was insufficient to promote a strong lactic fermentation, the addition of 20 to 30 kg molasses/tonne should achieve satisfactory preservation.M. Tjandraatmadja and B.W. Norton are with the Department of Agriculture, The University of Queensland, Queensland, 4072, Australia; I.C. Mac Rae is with the Department of Microbiology, The University of Queensland, Queensland, 4072, Australia.     

Development of starter culture for improved processing of Lafun,an African fermented cassava food product

Aims: To select appropriate micro‐organisms to be used as starter culture for reliable and reproducible fermentation of Lafun. Methods and Results: A total of 22 cultures consisting of yeast, lactic acid bacteria (LAB) and Bacillus cereus strains predominant in traditionally fermented cassava during Lafun processing were tested as potential starter cultures. In an initial screening, Saccharomyces cerevisiae 2Y48P22, Lactobacillus fermentum 2L48P21, Lactobacillus plantarum 1L48P35 and B. cereus 2B24P31 were found to be the most promising of the cultures and were subsequently tested in different combinations as mixed starter cultures to ferment submerged cassava roots. Saccharomyces cerevisiae, inoculated singly or combined with B. cereus, gave the softest cassava root after 48 h of fermentation according to determination of compression profile and stress at fracture. Overall, sensory quality testing showed that Lafun obtained from S. cerevisiae‐fermented cassava gave the most preferred stiff porridge. Saccharomyces cerevisiae 2Y48P22 showed pectinase production in a model system. Conclusions: The results suggest that S. cerevisiae 2Y48P22 is the most efficient organism for cassava softening during the fermentation. Therefore, it could be combined with LAB and used as starter for Lafun processing. Significance and Impact of the Study: Starter cultures are made available for controlled fermentation of Lafun.     

<Emphasis Type="SmallCaps">l</Emphasis>(+)-Lactic acid production from non-food carbohydrates by thermotolerant <Emphasis Type="Italic">Bacillus coagulans</Emphasis>

Lactic acid is used as an additive in foods, pharmaceuticals, and cosmetics, and is also an industrial chemical. Optically pure lactic acid is increasingly used as a renewable bio-based product to replace petroleum-based plastics. However, current production of lactic acid depends on carbohydrate feedstocks that have alternate uses as foods. The use of non-food feedstocks by current commercial biocatalysts is limited by inefficient pathways for pentose utilization. B. coagulans strain 36D1 is a thermotolerant bacterium that can grow and efficiently ferment pentoses using the pentose-phosphate pathway and all other sugar constituents of lignocellulosic biomass at 50°C and pH 5.0, conditions that also favor simultaneous enzymatic saccharification and fermentation (SSF) of cellulose. Using this bacterial biocatalyst, high levels (150–180 g l⁻¹) of lactic acid were produced from xylose and glucose with minimal by-products in mineral salts medium. In a fed-batch SSF of crystalline cellulose with fungal enzymes and B. coagulans, lactic acid titer was 80 g l⁻¹ and the yield was close to 80%. These results demonstrate that B. coagulans can effectively ferment non-food carbohydrates from lignocellulose to l(+)-lactic acid at sufficient concentrations for commercial application. The high temperature fermentation of pentoses and hexoses to lactic acid by B. coagulans has these additional advantages: reduction in cellulase loading in SSF of cellulose with a decrease in enzyme cost in the process and a reduction in contamination of large-scale fermentations.     

Effect of oxygen on batch yogurt cultures

A yogurt culture (Streptococcus thermophilus 15HA + Lactobacillus delbrueckii subsp. bulgaricus 2-11) was studied in conditions of aerobic batch fermentation (10–40% dissolved oxygen in milk). The growth and acidification of S. thermophilus 15HA were stimulated at 20% oxygen concentration and the lactic acid process in a mixed culture was shortened by 1 h (2.5 h for the aerobic culture and 3.5 h for the anaerobic mixed culture). Streptococcus thermophilus 15HA oxygen tolerance was significantly impaired at oxygen concentrations in the milk above 30%. Though S. thermophilus 15HA was able to overcome to some extent the impact of high oxygen concentration (40%), the lactic acid produced was insufficient to coagulate the milk casein (4.0 g lactic acid l⁻¹ in the mixed culture and 3.8 g lactic acid l⁻¹ in the pure culture). A dramatic decrease in the viable cell count of L. delbrueckii subsp. bulgaricus 2-11 in the pure and mixed cultures was recorded at 30% dissolved oxygen. This revised version was published online in July 2006 with corrections to the Cover Date.     

Characterization of anaerobic microbial culture with high acidogenic activity

The mixed cultures which were used were isolated from municipal sludge digesters, and the production of organic acids (acetic, propionic, butyric, etc.) from carbohydrates was tested. The behavior of the reference population (culture R) obtained directly from the sewage treatment plant, is compared to that obtained after three months in a plug-flow reactor (Gradostat fermentor) without pH control (culture A) and after six months with pH control (culture B). For culture B, the specific rate of acid production is related to the cell growth rate by (1/X)r_p= 17 µ + 1.6 with a maximal acid concentration of 40 g/liter. The batch culture yields are improved from 0.36g/g for the initial culture (R) to 0.72 g/g for culture B after six months in continuous culture, and 0.8 g/g in plug-flow continuous culture. The productivity of organic acids reaches 1.7 g/liter·hr. It is suggested that the acidogenic fermentation, the first step of methanogenesis, is a potential process to produce acetic, propionic, and butyric acids.     

Experiences with the use of a starter culture in the fermentation of maize for ‘kenkey’ production in Ghana

Controlled fermentation of maize was carried out using six strains of Lactobacillus fermentum and one strain of yeast, Saccharomyces cerevisiae, isolated from traditionally fermented maize dough as starter cultures for inoculum enrichement. The fermentations were monitored by pH, acidity, microbiological analysis and taste panel evaluation of two products, kenkey and koko, prepared from the fermented doughs. The strains of L. fermentum used as starter culture dominated the microflora during fermentation and in most inoculated doughs the required pH was attained by 24 h instead of 48 h of dough fermentation. Higher contents of lactic acid bacteria and yeasts were observed in inoculated doughs at the initial stages of fermentation but the spontaneously fermented doughs attained similar lactic acid bacteria and yeasts counts by 24 h of dough fermentation. The organoleptic quality of kenkey and koko prepared from doughs fermented with starter culture for 48 h was not significantly different from the traditional products. Kenkey prepared from doughs fermented for 24 h with starter culture were found to be unacceptable by the taste panel although similarly produced koko was acceptable.The authors are with the Food Research Institute, Council for Scientific and Industrial Research, P.O Box M 20. Accra, Ghana.     

Generalized model of the effect of pH on lactate fermentation and citrate bioconversion in Lactococcus lactis ssp. Lactis biovar. diacetylactis

An aroma-imparting mesophilic lactic starter (Lactococcus lactis ssp. lactis biovar. diacetylactis) was studied in batch culture in medium with 50 g·l^–1 lactose and 2 g·l^–1 citrate. The effect of pH on the physiology of growth and the production of flavour compounds was investigated with a mathematical model. The specific rates of growth and of lactose fermentation obeyed a law of non-competitive inhibition by lactic acid produced, inhibition increasing as the pH of the medium decreased. The pH thus acted indirectly by increasing the proportion of non-dissociated lactic acid, identified as the inhibiting form of lactic acid. The generalized model, taking into account the effect of pH, was tested using fermentations at pH controlled at different values (4.5–6.5), as well as with a fermentation conducted at non-regulated pH. These simulations supported the working hypotheses. The effect of pH on the fermentation of citric acid resulted in an increase in the maximal specific rate of citrate utilization, in the bioconversion yield, and in the constant of diacetyl and acetoin reduction at acid pH. The production of flavour compounds is a complex phenomenon resulting from the interaction of pH, citric acid concentration, and the physiological state of the cells. These results are discussed with respect to the use of this strain in the preparation of manufactured dairy products.     

Efficient conversion of lactic acid to butanol with pH-stat continuous lactic acid and glucose feeding method by Clostridium saccharoperbutylacetonicum

In order to achieve high butanol production by Clostridium saccharoperbutylacetonicum N1-4, the effect of lactic acid on acetone–butanol–ethanol fermentation and several fed-batch cultures in which lactic acid is fed have been investigated. When a medium containing 20 g/l glucose was supplemented with 5 g/l of closely racemic lactic acid, both the concentration and yield of butanol increased; however, supplementation with more than 10 g/l lactic acid did not increase the butanol concentration. It was found that when fed a mixture of lactic acid and glucose, the final concentration of butanol produced by a fed-batch culture was greater than that produced by a batch culture. In addition, a pH-controlled fed-batch culture resulted in not only acceleration of lactic acid consumption but also a further increase in butanol production. Finally, we obtained 15.5 g/l butanol at a production rate of 1.76 g/l/h using a fed-batch culture with a pH-stat continuous lactic acid and glucose feeding method. To confirm whether lactic acid was converted to butanol by the N1-4 strain, we performed gas chromatography–mass spectroscopy (GC-MS) analysis of butanol produced by a batch culture during fermentation in a medium containing [1,2,3-¹³C₃] lactic acid as the initial substrate. The results of the GC-MS analysis confirmed the bioconversion of lactic acid to butanol.     

Xylanase production in solid-state fermentation: a study of its properties

Summary Xylanase production by Aspergillus niger van Tieghem was studied in solid-state cultivation. The screening of substrates was carried out in column incubators aerated with humidified air at 30°C. Results of physiological studies showed that the best yield of xylanase was 2500 U/g dry matter on a mixture of straw+bran 1:1 at 70% of moisture content.In order to compare some properties of the xylanase produced in both liquid and solid cultures, A. niger was also grown on xylan in submerged cultures. The enzymes produced in solid and liquid cultures have an optimum pH of about 3.8 and 4.5, respectively. Xylanase synthetized in solid fermentation is a little more thermostable than that from liquid culture and is maximally active at 50° C, compared to 45° C for enzyme from liquid culture.     

Studies on Oxidation-Reduction Potentials (ORP) of Microbial Cultures

Aerobacter aerogenes No. 505 isolated from soil by Uyeda produced l-valine extracellularly by an aerobic shaking culture. Under anaerobic conditions the production of this amino acid was inhibited while lactic acid as well as a small amount of alanine were produced. The changes in ORP during the incubation under both conditions were investigated. When l-valine was the main product under aerobic conditions the ORP showed a constant value (rH 8.0) from 16 to 40 hr after inoculation. But when lactic acid was the main product and alanine was produced as the only amino acid under anaerobic conditions, the ORP drifted to rH 0 (zero). The phenomenon of the conversion of fermentation was shown clearly by the ORP of the culture broth.

The endpotentiai of lactic acid fermentation by Rhizopus G-36 was rH 13 to 14 when measured in the presence of trace amounts of redox dye mixtures. Without dyes, the rH was 18 to 22 and this fungal culture was slower in reaching endpotentials than bacterial cultures. It was postulated that the amount of redox substances exhibiting electromotive activity was not sufficient in this culture.

rH value 13 to 14 was not obtained under such conditions that lactic acid was not produced; that is in a medium with higher concentration of the nitrogen source in the presence of Fe²⁺ and Zn²⁺, or in a medium containing acetate in place of glucose as the carbon source.

Mycelia of Rhizopus G-36 after 36 hr-culture produced lactic acid even in the absence of oxygen. But unexpectedly, the ORP under anaerobic secondary culture was exactly the same as that in the aerobic shaking culture (rH 13.2).

A method for homogenization of the culture without secondary oxidation was improved. The ORP of anaerobically homogenized cultures was rH 11, and was thought to be due to the activities of all redox systems in the mycelium.

The respiration system of this strain was switched from cytochrome system to flavin system at the point of change in KGN-sensitivity. The ORP of this strain may be influenced by respiration through the flavin system.     

Kinetic study on pH dependence of growth and death of Streptococcus faecalis

A chemostat culture was used for lactic acid fermentation with Streptococcus faecalis at various pH values (8.0, 7.0, 6.0, 5.5, 5.0) and glucose concentrations (10, 20, 30 g/l). At every pH value, the reciprocals of the specific consumption rate of glucose and the specific production rate of lactic acid were linearly correlated to the reciprocal of the specific growth rate. The product, lactic acid, caused non-competitive inhibition of the specific growth rate at every pH value. Moreover, it was found that the cell death rate was dependent on pH and lactic acid. The death rate was smallest at pH 7.0 and increased with increasing lactic acid concentration. The kinetic equations of growth and death are proposed in a broader pH range. Correspondence to: H. Ohara     

Limitation of growth and lactic acid production in batch and continuous cultures of Lactobacillus helveticus

Summary Continuous and batch cultures of Lactobacillus helveticus operated under different conditions were studied with respect to the limitation of growth and lactic acid production by increasing undissociated lactic acid and hydrogen ion concentrations, respectively. In a single-stage continuous culture without pH control a final pH of 3.8 and 65 mm undissociated lactic acid was obtained. In two-stage continuous cultures provided with different growth media and run at different pH values, 65–70 mm free acid was obtained in the second stage. Further batch-culture experiments showed growth limitation at 60–70 mm lactic acid. After growth ceased, production of lactate continued until a lactic acid concentration of about 100 mm was reached; obviously an uncoupling of growth and acid production had occurred. Examining the effect of different concentrations of either lactic acid or hydrochloric acid, added to growing batch cultures of L. helveticus, it was shown that the undissociated lactic acid concentration was responsible for growth limitation and lactic acid production in this organism, whereas the pH value had only an indirect effect.     

Unstructured models for growth and lactic acid production during two-stage continuous cultures of Lactobacillus helveticus

During lactic acid fermentation, seed culture is usually carried out without pH control, while culture is carried out at pH controlled at the optimal value to overcome inhibitory effects. The Luedeking–Piret expression was therefore previously modified by introducing additional terms involving the undissociated form of the lactic acid, the main inhibitory species, in case of batch cultures without pH control or involving the residual lactose concentration to account for the carbon substrate limitation, responsible for cessation of production during batch cultures of Lactobacillus helveticus at controlled pH. Both expressions were also merged to deduce a generalized model. Both models, as well as the Luedeking–Piret model, were developed to describe continuous two-stage culture of L. helveticus. By considering the parameter values obtained from the fitting of batch culture data, both modified Luedeking–Piret models showed interesting predictive potential. Indeed, some rather reliable predictive calculated values were recorded in both stages; the residual standard deviations were 0.5 and less than 8.8 for the biomass and the product concentrations at steady-state in the culture stage (second stage). The optimization of the parameters for growth- and non-growth-associated parameters improved the fitting in the culture stage, leading to residual standard deviations below 2.6 for lactic acid concentrations at steady-state.     

Probiotication of tomato juice by lactic acid bacteria

This study was undertaken to determine the suitability of tomato juice as a raw material for production of probiotic juice by four lactic acid bacteria (Latobacillus acidophilus LA39, Lactobacillus plantarum C3, Lactobacillus casei A4, and Lactobacillus delbrueckii D7). Tomato juice was inoculated with a 24-h-old culture and incubated at 30 degrees C. Changes in pH, acidity, sugar content, and viable cell counts during fermentation under controlled conditions were measured. The lactic acid cultures reduced the pH to 4.1 or below and increased the acidity to 0.65% or higher, and the viable cell counts (CFU) reached nearly 1.0 to 9.0 x 10(9)/ml after 72 h fermentation. The viable cell counts of the four lactic acid bacteria in the fermented tomato juice ranged from 10(6) to 10(8) CFU/ml after 4 weeks of cold storage at 4 degrees C. Probiotic tomato juice could serve as a health beverage for vegetarians or consumers who are allergic to dairy products.     

Direct fermentation of potato starch wastewater to lactic acid by Rhizopus oryzae and Rhizopus arrhizus

The biochemical kinetic of direct fermentation for lactic acid production by fungal species of Rhizopus arrhizus 3,6017 and Rhizopus oryzae 2,062 was studied with respect to growth pH, temperature and substrate. The direct fermentation was characterized by starch hydrolysis, accumulation of reducing sugar, and production of lactic acid and fungal biomass. Starch hydrolysis, reducing sugar accumulation, biomass formation and lactic acid production were affected with the variations in pH, temperature, and starch source and concentration. A growth condition with starch concentration approximately 20 g/l at pH 6.0 and 30°C was favourable for both starch saccharification and lactic acid fermentation, resulting in lactic acid yield of 0.87–0.97 g/g starch associated with 1.5–2.0 g/l fungal biomass produced in 36 h fermentation. R. arrhizus 3,6017 had a higher capacity to produce lactic acid, while R. oryzae 2,062 produced more fungal biomass under similar conditions.